A solar thermochemical reactor includes an outer member, an inner member disposed within an outer member, wherein the outer member surrounds the inner member and wherein the outer member has an aperture for receiving solar radiation and wherein an inner cavity and an outer cavity are formed by the inner member and outer member and a reactive material capable of being magnetically stabilized wherein the reactive material is disposed in the outer cavity between the inner member and the outer member.
|
1. A method of using a solar thermochemical reactor comprising:
providing a solar thermochemical reactor including an outer member;
disposing an inner member within the outer member, wherein the outer member surrounds the inner member;
disposing a reactive material capable of being magnetically stabilized in between the outer member and the inner member;
applying a vacuum to the outer member after disposing the reactive material;
fluidizing the reactive material after applying the vacuum;
applying a magnetic field around the outer member after fluidizing the reactive material;
causing solar radiation to be received by the outer member while the magnetic field is applied;
carrying out a reduction reaction in the reactor to produce oxygen, the reduction reaction being carried out after causing the solar radiation to be received;
extracting the oxygen from the outer member;
disposing carbon dioxide and water onto the reactor material after extracting the oxygen;
carrying out an oxidation reaction in the reactor to produce carbon monoxide gas and hydrogen gas; and
extracting carbon monoxide gas and hydrogen gas from the outer member.
2. The method of
3. The method of
4. The method of
|
|||||||||||||||||||||||||||||||||||
This application claims the benefit of US National Stage application Ser. No. 14/367,495, filed Jun. 20, 2014, which claims the benefit of International Application No. PCT/US2012/071332, filed on Dec. 21, 2012, which claims the benefit of U.S. Application No. 61/579,449, filed on Dec. 22, 2011, which is incorporated herein by reference in their entirety.
This invention was made with Government support under DE-AR0000184 awarded by the U.S. Department of Energy. The Government has certain rights in this invention.
This disclosure relates to a solar thermochemical reactor, methods of manufacture, and uses thereof and a thermogravimeter.
Solar thermochemistry is a newly emerging technology for the production of fuels using highly concentrated solar radiation. Solar power is used to facilitate thermochemical reactions. Solar thermochemical reactors are in the early stages of development. Significant challenges are posed by the use of solar energy as a renewable energy source, which makes it difficult to deploy on a large scale. Solar energy is, by its nature, transient as it is dependent upon exposure to the sun. Solar thermochemical reactions can proceed at very high temperatures. Solar chemical reactors can also employ a window manufactured from an optically transparent material (e.g., glass, plastic, or combinations thereof) to admit highly concentrated radiation to the reaction site. The optically transparent material can be structurally weak and extremely susceptible to staining and subsequent damage due to thermal stresses. In addition, thermochemical reactions can result in sintering of the reactant materials that reduces their internal surface area and adversely affects the chemical kinetics of the reaction.
It is therefore desirable to develop solar thermochemical reactors which operate under lower temperature conditions, do not use a window that is manufactured from an optically transparent material and facilitate control of the chemical kinetics of the thermochemical reaction. It is also desirable to develop a method of using solar thermochemical reactors in a manner which maximizes the availability of solar energy during non-transient periods.
Disclosed herein is a solar thermochemical reactor comprising an outer member, an inner member disposed within and surrounded by the outer member, wherein the outer member has an aperture for receiving solar radiation, an inner cavity and an outer cavity formed by the inner and outer members, respectively, and a reactive material capable of being magnetically stabilized wherein the reactive material is disposed in the outer cavity between the inner member and the outer member.
Disclosed herein too is a method of making a solar thermochemical reactor comprising disposing an inner member within an outer member that surrounds the inner member wherein the outer member has an aperture for receiving solar radiation and disposing a reactive material capable of being magnetically stabilized between the inner member and the outer member.
Disclosed herein too is a method of using a solar thermochemical reactor comprising disposing an inner member within an outer member, wherein the outer member surrounds the inner member, disposing a reactive material capable of being magnetically stabilized in between the outer member and the inner member, applying a vacuum to the outer member, fluidizing the reactive material, applying a magnetic field at least partially around the outer member; disposing solar radiation onto the outer member, carrying out a reduction reaction in the reactor, extracting oxygen from the outer member; disposing carbon dioxide and water onto the reactor material, carrying out an oxidation reaction in the reactor and extracting carbon monoxide gas and hydrogen gas from the outer member.
Disclosed herein too is a cycling loop process for producing synthetic gas comprising disposing a first solar thermochemical reactor in close proximity to a second solar thermochemical reactor, focusing solar radiation from a concentrated source onto the first solar thermochemical reactor, carrying out a reduction reaction in the first solar thermochemical reactor, focusing solar radiation from the concentrated source onto a second solar thermochemical reactor, and carrying out a reduction reaction in the second solar thermochemical reactor wherein the first reactor and second reactor each comprise an outer member having an aperture for receiving solar radiation, wherein said outer member completely surrounds an inner member, wherein the outer member and inner member form an inner cavity and outer cavity and further wherein a reactor material capable of becoming magnetically stabilized is disposed in the outer cavity.
Disclosed herein too is a solar thermogravimeter for modeling the kinetics of thermochemical reactions in a solar thermochemical reactor comprising a metal pressure vessel, a tubular or dome shaped quartz vessel for optical access, a low vibration vacuum pump, an analytical balance disposed within the low pressure vessel, a temperature sensor, a thermocouple, a flow meter and a gas phase chromatograph or mass spectrometer.
It will be understood that when an element is referred to as being “on” another element, it can be directly on the other element or intervening elements may be present therebetween. In contrast, when an element is referred to as being “directly on” another element, there are no intervening elements present. As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed items.
It will be understood that, although the terms first, second, third, etc. may be used herein to describe various elements, components, regions, layers and/or sections, these elements, components, regions, layers and/or sections should not be limited by these terms. These terms are only used to distinguish one element, component, region, layer or section from another element, component, region, layer or section. Thus, a first element, component, region, layer or section discussed below could be termed a second element, component, region, layer or section without departing from the teachings of the present invention.
The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting. As used herein, the singular forms “a,” “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “comprises” and/or “comprising,” or “includes” and/or “including” when used in this specification, specify the presence of stated features, regions, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, regions, integers, steps, operations, elements, components, and/or groups thereof.
Furthermore, relative terms, such as “lower” or “bottom,” “upper” or “top,” and “inner” or “outer” may be used herein to describe one element's relationship to another element as illustrated in the Figures. It will be understood that relative terms are intended to encompass different orientations of the device in addition to the orientation depicted in the figures. For example, if the device in one of the figures is turned over, elements described as being on the “lower” side of other elements would then be oriented on “upper” sides of the other elements. The exemplary term “lower,” can therefore, encompass both an orientation of “lower” and “upper,” depending on the particular orientation of the figure. Similarly, if the device in one of the figures is turned over, elements described as “below” or “beneath” other elements would then be oriented “above” the other elements. The exemplary terms “below” or “beneath” can, therefore, encompass both an orientation of above and below.
Unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and the present disclosure, and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.
Exemplary embodiments are described herein with reference to cross section illustrations that are schematic illustrations of idealized embodiments. As such, variations from the shapes of the illustrations as a result, for example, of manufacturing techniques and/or tolerances, are to be expected. Thus, embodiments described herein should not be construed as limited to the particular shapes of regions as illustrated herein but are to include deviations in shapes that result, for example, from manufacturing. For example, a region illustrated or described as flat may, typically, have rough and/or nonlinear features. Moreover, sharp angles that are illustrated may be rounded. Thus, the regions illustrated in the figures are schematic in nature and their shapes are not intended to illustrate the precise shape of a region and are not intended to limit the scope of the present claims.
The transition term “comprising” encompasses the transition terms “consisting of” and “consisting essentially of.”
Various numerical ranges are disclosed herein. These ranges are inclusive of the endpoints as well as numerical values between these endpoints. The numbers in these ranges and those on the endpoints are interchangeable.
Solar energy is the most abundant source of renewable energy. Because solar energy is an intermittent power source, storage of this energy is desirable for large-scale deployment and production of fuels. Solar thermochemistry can be used to produce synthetic gas (“syngas”), a precursor used for the production of clean and carbon neutral synthetic hydrocarbon fuels such as methanol, methane or synthetic petroleum. Solar thermochemistry can also be used to store concentrated solar energy in chemical energy carriers until production of syngas or fuel is desired. Thermochemical storage of concentrated solar energy is desirable because chemical energy carriers have a high energy density, are stable, can be stored indefinitely; and a complete infrastructure for their transport and storage already exists, i.e., the existing infrastructure for hydrocarbon fuel transport and storage.
Solar thermochemical reactors can have windowed in which the window is manufactured from an optically transparent material. Such windowed designs present reliability issues due to weakness in mechanical structure and staining and limit the size of reactors, making it difficult to scale up solar reactor technology to an industrial level. In addition, metal reactor materials used in solar thermochemical reactors can be subject to undesirable sintering, which reduces the surface area of the metal reactor materials and causes the period during which the metal reactor materials are used for repeated reactor reaction cycles to become significantly reduced. The thermochemical reactions which are carried out in solar reactors also involve significant periods of time. For example, a single cycle to produce syngas using reduction and oxidation can take up to five hours.
Two-step metal oxide looping processes involve a reduction reaction and an oxidation reaction to complete one “redox” cycle. The direct thermolysis of water can involve temperatures in excess of 2500° C. Two-step metal oxide looping processes can be advantageous because they avoid these extreme temperatures. Two-step metal oxide looping processes using volatile metal oxides such as zinc oxide can have disadvantages associated with avoiding recombination of the highly reactive gaseous metal-oxygen mixture produced. Such processes can also involve high temperatures to carry out the solar reduction/metal disassociation step.
Disclosed herein are reactors, methods of manufacture and use thereof and thermogravimeters which address one or more of the above-described challenges. Disclosed herein is a solar thermochemical reactor comprising an outer member, an inner member disposed within and surrounded by the outer member, wherein the outer member has an aperture for receiving solar radiation, an inner cavity and an outer cavity formed by the inner and outer members, respectively and a reactive material capable of being magnetically stabilized wherein the reactive material is disposed in the outer cavity between the inner member and the outer member.
Disclosed herein too is a method of making a solar thermochemical reactor comprising disposing an inner member disposed within an outer member that surrounds the inner member wherein the outer member has an aperture for receiving solar radiation and disposing a reactive material capable of being magnetically stabilized between the inner member and the outer member.
In an exemplary embodiment, as depicted in
The use of an aperture 40 with the dual cavity design overcomes the structural weakness and efficiency problems associated with the use of optically transparent materials (e.g., glass, plastic, or combinations thereof) in windows in reactor systems. Accordingly, the reactor 10 has an aperture 40 which is devoid of an optically transparent material. In an embodiment, the aperture 40 comprises a media that has a refractive index of about 1.0 to about 1.05. In another embodiment, the aperture 40 comprises a media that has a density of about 0.90 to about 1.50 kg/m3. In yet another embodiment, the aperture 40 comprises a fluid. In an exemplary embodiment, the aperture 40 comprises a fluid wherein the fluid is air.
In another exemplary embodiment, as depicted in
In an embodiment, the outer member 20 further comprises a shutter which exposes or covers the aperture 40 in the outer member 20 for receiving solar radiation as desired. The shutter 120 can be seen in the
Referring back to
The dual cavity design of the reactor 10 maximizes the effective absorbance of solar radiation in the reactor 10 and minimizes re-radiation losses. The use of a vacuum reduces the temperatures used to carry out thermochemical reduction reactions in the solar thermochemical reactor 10.
In another exemplary embodiment, as depicted in a cross section of the reactor assembly shown in
The reactor material 70 comprises particles which are capable of becoming magnetically stabilized. Exemplary materials are described in detail in U.S. Provisional Patent Application No. 61/505,890 filed on Jul. 8, 2011, which is incorporated by reference in its entirety herein. Specifically, exemplary reactor materials 70 include metal oxides such as iron, iron oxides or mixtures thereof. More specifically, exemplary reactor materials 70 are selected from the group consisting of Fe2O3, Fe3O4, and NiFe2O4 or a combination including at least one of the foregoing. In an embodiment, the metal oxide reactor materials 70 are non-volatile. Another group of exemplary reactor materials 70 are carbonaceous materials. An example of such carbonaceous materials are activated carbon. Activated carbon is also called activated charcoal or activated coal and is a form of carbon that is riddled with small, low-volume pores that increase the surface area available for adsorption or chemical reactions. The activated carbon is mixed into ferrite powder and oxidized using either air or steam to form the reactor material 70. During the oxidation, the activated carbon is converted from a solid to a gas, i.e., from carbon to carbon dioxide. Since the activated carbon is all converted to carbon dioxide during the oxidation, the resulting reactor material contains only the oxidized porous ferrite powder. Non-volatile metal oxides, when used solar thermochemical reactions, avoid undesirable properties associated with volatile metal oxides associated with rapid quenching.
The reactor materials 70 form a bed of reactor materials within the outer cavity 60. The bed of reactor materials is then fluidized. When a magnetic field is applied to the outer member 20, and solar radiation is disposed upon the aperture 40, the temperature is elevated, and the bed of reactor materials 70 becomes magnetically stabilized. Iron powder sinters at 550° C. when oxidized. Therefore, the magnetically stabilized bed is sintered at a relatively low temperature. This results in sintering of the reactor materials 70 into a state in which the surface area is not substantially reduced. The exposure to a magnetic field has the effect of freezing the reactor materials 70 into a structure with a high surface area. The particle chains within the reactor materials 70 repel each other due to the magnetic force, creating a high surface area structure with high porosity which can withstand exposure to relatively high temperatures during the first reduction reaction of the redox cycle. In an embodiment, the magnetic field is only used during synthesis of the magnetically stabilized bed structure prior to the first reduction reaction carried out in the solar reactor using the reactor materials 70. The magnetically stabilized bed of reactor materials can overcome the sintering problems associated with other reactive materials which become sintered such that the surface area is reduced, and therefore undergo favorable chemical kinetics during reactor cycles. Accordingly, the reactor materials 70 disclosed herein avoid deactivation due to undesirable sintering and are capable of being used for many repeated reaction cycles in the reactor 10 without requiring new reactor materials to be loaded into the reactor.
The dual cavity design of the reactor 10 and magnetically stabilized reactor materials 70 used therein are used at relatively low pressures, thereby overcoming the challenges of other reactor systems which use high temperatures and high pressures. The reaction temperatures in the reduction reaction are lowered by lowering the partial pressure of the oxygen evolving as a result of the reaction. The low pressure utilized also allows for lower temperature conditions for carrying out the reduction reaction in the reactor 10. In an exemplary embodiment, the dual cavity solar thermochemical reactor 10 is operated at partial oxygen pressures of less than about 10−4 bar, specifically less than 10−3 bar, and more specifically less than 5×10−4 bar to facilitate the disassociation of the metal in the reactor material 70. In another exemplary embodiment, the dual cavity solar thermochemical reactor may be operated at temperatures of less than 1500° C., specifically less than 1500° C., and more specifically less than 1450° C. In another embodiment, the dual cavity design of the reactor 10 has a low thermal mass and is equipped with a control system to control irradiation in order to cope with transient periods of availability of solar radiation. In addition, waste heat from the reactor discharge gases are recouped, and transferred to the inlet reactants, H2O and CO2, to increase energy conversion efficiency.
Fracturing, caused by matrix mismatch or spallation of the metal oxide reactor material 70 is controlled by controlling the growth conditions, specifically the film thickness and/or rate of growth. In another embodiment, short duration redox cycles are used to avoid spallation and fracture. In yet another embodiment, use of a magnetically stabilized fluidized bed of reactor materials 70 avoids fracturing and spallation.
Disclosed herein too is a method of using a solar thermochemical reactor comprising disposing an inner member within an outer member, wherein the outer member surrounds the inner member, disposing a reactive material capable of being magnetically stabilized in between the outer member and the inner member, applying a vacuum to the outer member, fluidizing the reactive material, applying a magnetic field at least partially around the outer member; disposing solar radiation onto the outer member, carrying out a reduction reaction in the reactor, extracting oxygen from the outer member; disposing carbon dioxide and water onto the reactor material, carrying out an oxidation reaction in the reactor and extracting carbon monoxide gas and hydrogen gas from the outer member.
As depicted in
Fe3O4+solar heat→3FeO+0.5O2
Fe2O3+solar heat→2FeO+0.5O2
NiFe2O4+solar heat→NiFe2O3+0.5O2
In an embodiment, the reduction of reactive materials 70 in the solar thermochemical reactor 10 results in reduction to iron, although this is less probable than the equations represented above, and is represented by the following exemplary chemical equation:
Fe3O4+solar heat→3Fe+2O2
In an exemplary embodiment, as depicted in
After the thermochemical reduction reaction is complete, the shutter 120 is closed, preventing solar radiation from entering the aperture 40 of the outer member 20. The reactor 10 is then used to carry out a thermochemical oxidation reaction in oxidation mode. The closed shutter 120 allows heat generated in the reactor to be retained and helps to minimize radiation loss.
In an exemplary embodiment, as depicted in
3FeO+H2O+CO2→Fe3O4+H2+CO
2FeO+H2O+CO2→Fe2O3+H2+CO
3Fe+4H2O+CO2→Fe3O4+4H2+CO
2NiFe2O3+H2O+CO2→2NiFe2O4+H2+CO
The thermochemical reduction reaction and oxidation reaction together constitute a single redox cycle. The resulting syngas is refined into fuel for commercial use or stored for later refinement. In an embodiment, the magnetically stabilized bed material is used for many cycles, specifically many hundred cycles, and more specifically thousands of cycles, before being replaced. In another embodiment, the redox reactions are carried out in short duration cycles. For example, a complete redox cycle is carried out in about one hour, more specifically in about 15 minutes.
In yet another exemplary embodiment, a looping process is provided as depicted in
Two or more reactors in close proximity to one another are used in the looping process. In one embodiment, at least two reactors are disposed side-by-side. In another embodiment, at least one reactor is disposed on top of at least one other reactor. In another embodiment, the shifting of the solar radiation onto to reactor is accomplished by shifting a heliostat to move the concentrated solar radiation from one reactor to another. In another embodiment, two or more reactors are disposed upon a rotating reactor assembly which refocuses concentrated solar radiation from one reactor to another. In yet another embodiment, a beam-redirected mirror is used to refocus concentrated solar radiation from one reactor to another.
In an exemplary embodiment, a solar reactor having a dual cavity design as described above has an aperture 40 that does not include an optically transparent material, operates at a relatively a low pressure and temperature to carry out the metal dissociation reduction step, and magnetically stabilized reactor materials are sintered in a controlled manner to avoid undesirable sintering and deactivation of the metal reactor materials.
In another embodiment, as depicted in
The reactor system 150 further comprises a heat exchanger 180 disposed upstream from and in fluid communication with the first solar thermochemical reactor 10 and the second solar thermochemical reactor 15. A second controller 190 is disposed upstream of the heat exchanger 180 from which carbon dioxide is supplied. The second controller 190 controls the flow rate of carbon dioxide supplied to the heat exchanger 180. In an embodiment, the flow rate of the carbon dioxide entering the heat exchanger 180 is from about 0.1 g-cm2 to about 1.0 g-cm2. The heat exchanger 180 elevates the temperature of the carbon dioxide supplied from second controller 190. The temperature in the heat exchanger 180 which is used to elevate the temperature of the carbon dioxide is from about 25° C. to about 400° C. The carbon dioxide is then supplied from the heat exchanger 180 to the first solar thermochemical reactor 10 and the second solar thermochemical reactor 15 for use in the redox cycle reactions carried out therein.
The reactor system 150 further comprises means for heat recuperation. A first vacuum pump 192 and a second vacuum pump 194 are disposed downstream of and in fluid communication with the first solar thermochemical reactor 10 and the second solar thermochemical reactor 15. The first vacuum pump 192 and second vacuum pump 194 remove oxygen produced from the redox cycle reactions which occur in the reactors. Heat generated from the redox cycle reactions carried out in the first solar thermochemical reactor 10 and the second solar thermochemical reactor 15, and the hydrogen and carbon monoxide reaction products, are supplied to the steam generator 160 where the heat is used to generate steam from water. The heat is supplied from the steam generator 160 to the heat exchanger 180 where the heat is used to elevate the temperature of the carbon dioxide reaction product and the reaction products are collected. In another embodiment, the reactor system 150 also includes other heat recuperation technology.
Disclosed herein too is a solar thermogravimeter for modeling the kinetics of thermochemical reactions in a solar thermochemical reactor. The thermogravimeter facilitates modeling of thermochemical reactions to optimize reaction conditions and increase efficiency of operations in a solar reactor.
In an exemplary embodiment, a thermogravimeter is assembled as shown in
The invention is exemplified by the following non-limiting examples.
As shown in
The output from a thermogravimeter demonstrating the cyclic reactivity for three redox cycles is shown in
This example was conducted to demonstrate the manufacturing of the monolithic solid (reactor bed materials 70—referring to the
To test this approach, a 0.1 g sample of the activated carbon was tested in a thermogravimeter and oxidized using a flow of 100 cubic centimeters of air during a temperature ramp to 1000° C. at 5° C./min. The results of this test are seen in the
It can be seen above that the onset of oxidation occurs at approximately 500° C. and rapid mass loss proceeds. While the
The procedure for making a porous structure (i.e., the monolithic solid) is as follows. Ferrite powder (crushed and sieved to 75 to 125 micrometer size) and activated carbon (as received, Fisher Chemical, catalog number C272500) are mixed thoroughly together and placed into a quartz tube reactor. The mixture is then slowly heated (10° C./min) using an inert gas (Nitrogen/Argon) to 1000° C. The mixture is then reduced using a reducing gas (5% H2 in Ar) to bring the ferrite powder to its lowest oxidation state. This procedure has no effect on the activated carbon (already fully reduced). Following this, the powders are then oxidized using steam at low flow rates at the same temperature as reduction (1000-1200° C.). This allows for the oxidation of both the ferrite powder (Fe to Fe3O4, Co to Co3O4) and the activated carbon (C to CO2). However, since the activated carbon becomes a gas and the ferrite powder sinters, the resulting structure after oxidation is a porous monolithic solid in a ferrite matrix. The voids exist where the activated carbon once had been. Images of a resulting ACOS structure are shown below in
From this example, it may be seen that the activated carbon may be consumed or converted during the formation of the monolithic solid. Thus the monolithic solid may comprise a plurality of porous ferrite particles that are bonded together. In one embodiment, the activated particles can be consumed after the formation of the monolithic solid, leaving behind a porous monolithic solid that comprises only a plurality of ferrite particles that are lightly bonded together.
While the disclosure has been described with reference to exemplary embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the disclosure. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the disclosure without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this disclosure.
Klausner, James F., Petrasch, Joerg
| Patent | Priority | Assignee | Title |
| Patent | Priority | Assignee | Title |
| 4030890, | Oct 20 1975 | Solar power system | |
| 4115927, | Oct 11 1974 | Exxon Research & Engineering Co. | Process for operating a magnetically stabilized fluidized bed |
| 4292171, | Nov 01 1976 | Exxon Research & Engineering Co. | Magnetically stabilized, fluidized beds |
| 4319893, | Sep 02 1980 | Exxon Research & Engineering Co. | Magnetically stabilized bed, temperature, partial pressure swing, hydrogen recovery process |
| 4430254, | Feb 07 1979 | Ammonia Casale S.A. | Spherical cerium-activated catalyst for ammonia synthesis and process for its manufacture |
| 5143668, | Oct 06 1988 | Benchmark Structural Ceramics Corporation | Process for making a reaction-sintered carbide-based composite body with controlled combustion synthesis |
| 5863850, | Sep 21 1995 | PANASONIC HEALTHCARE CO , LTD | Process of making zirconia based ceramic material |
| 6633042, | Feb 25 2000 | DLR, DEUTSCHES ZENTRUM FUR LUFT-UND RAUMFAHRT E V | Solar photoreactor |
| 6780457, | Dec 28 1999 | Alstom Technology Ltd | Method for producing a high-quality insulation of electrical conductors or conductor bundles of rotating electrical machines by means of fluidized-bed sintering |
| 7033570, | May 08 2000 | Alliance for Sustainable Energy, LLC | Solar-thermal fluid-wall reaction processing |
| 7140181, | Mar 01 2002 | SUNDROP FUELS, INC | Reactor for solar processing of slightly-absorbing or transparent gases |
| 8110174, | Sep 07 2004 | NIIGATA UNIVERSITY | Reactive working material for use in hydrogen production by decomposition of water |
| 8187731, | May 05 2010 | The Regents of the University of Colorado | Metal ferrite spinel energy storage devices and methods for making and using same |
| 8388706, | Nov 16 2007 | Method using solar energy, microwaves and plasmas to produce a liquid fuel and hydrogen from biomass or fossil coal | |
| 20030208959, | |||
| 20050175533, | |||
| 20060229476, | |||
| 20080089834, | |||
| 20080236389, | |||
| 20090142578, | |||
| 20090232725, | |||
| 20100140154, | |||
| 20100303692, | |||
| 20110048690, | |||
| 20110136027, | |||
| 20120295113, | |||
| 20120302436, | |||
| 20130266502, | |||
| 20140291570, | |||
| 20150321158, | |||
| DE2735767, | |||
| JP10279955, | |||
| KR20110037329, | |||
| KR20110077154, | |||
| WO2010041014, | |||
| WO3004942, | |||
| WO3076334, | |||
| WO9600125, |
| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
| Jan 06 2012 | KLAUSNER, JAMES F | UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INC | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 045521 | /0615 | |
| Jan 06 2012 | KLAUSNER, JAMES F | UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INC | CORRECTIVE ASSIGNMENT TO CORRECT THE THE NAME OF JORG PETRASCH TO JOERG PETRASCH PREVIOUSLY RECORDED ON REEL 045521 FRAME 0615 ASSIGNOR S HEREBY CONFIRMS THE ASSIGNMENT | 047901 | /0476 | |
| Jan 13 2012 | PETRASCH, JORG | UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INC | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 045521 | /0615 | |
| Dec 20 2016 | University of Florida Research Foundation, Inc. | (assignment on the face of the patent) | / | |||
| Aug 08 2018 | PETRASCH, JOERG | UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INC | CORRECTIVE ASSIGNMENT TO CORRECT THE THE NAME OF JORG PETRASCH TO JOERG PETRASCH PREVIOUSLY RECORDED ON REEL 045521 FRAME 0615 ASSIGNOR S HEREBY CONFIRMS THE ASSIGNMENT | 047901 | /0476 |
| Date | Maintenance Fee Events |
| Jun 03 2022 | M2551: Payment of Maintenance Fee, 4th Yr, Small Entity. |
| Date | Maintenance Schedule |
| Mar 26 2022 | 4 years fee payment window open |
| Sep 26 2022 | 6 months grace period start (w surcharge) |
| Mar 26 2023 | patent expiry (for year 4) |
| Mar 26 2025 | 2 years to revive unintentionally abandoned end. (for year 4) |
| Mar 26 2026 | 8 years fee payment window open |
| Sep 26 2026 | 6 months grace period start (w surcharge) |
| Mar 26 2027 | patent expiry (for year 8) |
| Mar 26 2029 | 2 years to revive unintentionally abandoned end. (for year 8) |
| Mar 26 2030 | 12 years fee payment window open |
| Sep 26 2030 | 6 months grace period start (w surcharge) |
| Mar 26 2031 | patent expiry (for year 12) |
| Mar 26 2033 | 2 years to revive unintentionally abandoned end. (for year 12) |